| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_af99df08b153738cd418446a75d09bfc |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00155
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00166
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00033
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-1948
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-1942
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-0004
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00159 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-18
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-2415 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-18 |
| filingDate |
1997-10-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate |
1999-12-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b94e8f45329be7b9bd872829b35ec531
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_39a368159e8e3546d7fe856ed237be03
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f40db296658e16cea96ad7927eaebf39 |
| publicationDate |
1999-12-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
US-6004517-A |
| titleOfInvention |
Process to make allyl chloride and reactor useful in that process |
| abstract |
Allyl halide is produced in high yields and purity with minimal carbon formation using a process of: (1) initially reacting propylene and molecular halogen in a molar ratio of at least about 2.5:1 in a "continuously stirred tank reactor" (CSTR) zone under conditions suitable to provide a reaction temperature of about 400° C. to 525° C. to partially convert propylene and chlorine into allyl chloride; and (2) feeding an effluent from Step (1) into a plug-flow reactor zone where the reaction is continued at a temperature of about 400° C. to 525° C. until essentially all of the chlorine is consumed. A preferred reactor for the process contains: (1) a spherical, egg-shaped or oval reactor zone; (2) a tubular reactor zone attached to the spherical, egg-shaped or oval reactor zone; (3) one or more inlets for injecting gaseous reagents into the spherical, oval or egg-shaped reactor zone; and (4) one or more outlets from the tubular reactor zone for withdrawing a gaseous product. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2010067323-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-7097347-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-7422676-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-7115192-B1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2006096869-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2004100861-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8740448-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-6655829-B1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2006131161-A1 |
| priorityDate |
1995-05-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |